EP0892009B1 - Auf Polyethylene basierende Zusammensetzung sowie Verfahren zur Herstellung von Gegenständen aus dieser Zusammensetzung - Google Patents
Auf Polyethylene basierende Zusammensetzung sowie Verfahren zur Herstellung von Gegenständen aus dieser Zusammensetzung Download PDFInfo
- Publication number
- EP0892009B1 EP0892009B1 EP98202267A EP98202267A EP0892009B1 EP 0892009 B1 EP0892009 B1 EP 0892009B1 EP 98202267 A EP98202267 A EP 98202267A EP 98202267 A EP98202267 A EP 98202267A EP 0892009 B1 EP0892009 B1 EP 0892009B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- polyethylene
- composition according
- talc
- based composition
- composition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
- B29D23/00—Producing tubular articles
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethene
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L9/00—Rigid pipes
- F16L9/12—Rigid pipes of plastics with or without reinforcement
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/005—Additives being defined by their particle size in general
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
- C08L23/0815—Copolymers of ethene with aliphatic 1-olefins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S138/00—Pipes and tubular conduits
- Y10S138/07—Resins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
- Y10T428/139—Open-ended, self-supporting conduit, cylinder, or tube-type article
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
- Y10T428/269—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension including synthetic resin or polymer layer or component
Definitions
- the present invention relates to a composition based on polyethylene, a process for manufacturing shaped objects and the shaped objects from this composition. It relates more particularly to a composition based on high density polyethylene containing small amounts of a mineral additive finely divided and the objects fashioned from this composition, in particular tubes intended for the transport of fluids and, in particular, fluids under pressure.
- the present invention aims to provide a composition based on high density polyethylene which has resistance to hydrostatic pressure and therefore significantly improved creep resistance.
- the invention relates to a composition based on polyethylene according to claim 1.
- the talc which can be used in the compositions according to the invention can be any hydrated magnesium silicate of natural origin of general formula 3MgO. 4SiO 2 .H 2 O. It may contain minor amounts of metal oxides such as aluminum, iron and calcium oxides.
- the talc has an essentially lamellar texture. Its particle size distribution is preferably between 0.2 and 15 microns and its average particle size between 1 and 5 microns.
- the present invention results from the surprising observation that the addition small amounts of talc, less than 1 part by weight per 100 parts by weight of high density polyethylene, provides compositions which allow the manufacture of shaped objects such as tubes whose creep resistance is significantly improved without affecting the other mechanical properties of said artifacts, such as resistance to slow crack propagation ("stress cracking" or ESCR).
- polyethylene is meant to denote for the purposes of the present invention both homopolymers of ethylene and its copolymers with one or more several monomers and their mixtures.
- the usable comonomers may mention linear or branched olefins containing from 3 to 8 atoms of carbon, such as for example butene, hexene and 4-methylpentene, as well that diolefins comprising from 4 to 18 carbon atoms, such as 4-vinylcyclohexene, dicyclopentadiene, 1,3-butadiene, etc.
- the preferred comonomers are butene and hexene.
- the total content of comonomer (s) in the copolymer of ethylene amounts to at least 0.01 mol% and most often to 0.05 mol% at least.
- the total amount of comonomer (s) usually does not exceed 10% molar and most often 5% molar.
- ethylene copolymers containing in total from 0.05 to 5 mol% and more particularly still from 0.3 to 2 mol% of butene and / or hexene.
- ethylene copolymers advantageously used work in the compositions according to the invention, mention may be made of the co- and random terpolymers of ethylene and butene and / or hexene or the bimodal molecular weight copolymers obtained by block polymerization of mixtures of ethylene and butene and / or hexene. Bimodal distribution copolymers obtained by block polymerization ethylene and a mixture of ethylene and butene are particularly suitable well.
- polyethylene is used whose standard density as defined above is at least equal to 943 kg / m 3 and more particularly still to 946 kg / m 3 .
- the standard density does not exceed 960 kg / m 3 and more particularly still 955 kg / m 3 .
- the polyethylene used in the composition according to the invention is further characterized by a melt index, measured at 190 ° C, under a load of 5 kg according to ISO 1133 (1991) of at least 0.07g / 10min, values of at least 0.1g / 10min being the most common.
- the melt index generally does not exceed 5g / 10 min and most often does not 2 g / 10min.
- the composition according to the present invention can comprise usual additives for ethylene polymers, such as stabilizers (for example example of anti-acids, anti-oxidants and / or anti-UV) and agents implementation ("processing aid").
- stabilizers for example example of anti-acids, anti-oxidants and / or anti-UV
- processing aid agents implementation
- the content of the composition in each of these additives is generally less than 1%, preferably less than 0.5%, in weight.
- the composition according to the invention can also comprise pigments. Most often, the pigment content does not exceed 5% by weight of the composition and, more particularly still 3% by weight.
- composition according to the invention generally comprises at least 94%, preferably at least 96% by weight of polyethylene.
- the mode of preparation of the composition according to the invention is not critical. This can be obtained by any suitable known means.
- a preferred alternative method is to mix the polyethylene with the talc and the usual additives at temperature room temperature, and then mix them at a temperature higher than the temperature polyethylene, for example in a mechanical mixer or a extruder.
- Talc content of this masterbatch is generally from 0.5 to 5% by weight, preferably from 0.5 to 2% by weight and, more particularly from 0.75 to 1.5% by weight.
- This masterbatch is then mixed with the remaining fraction of polyethylene.
- These methods allow the composition to be obtained in the form of a powder which can be optionally then subject to granulation to obtain the composition to the state of granules. In known manner, these granules are obtained by extrusion of the composition by cutting the rod emerging from the extruder into granules.
- the process granulation can be done by feeding an extruder with a mixture previously prepared polyethylene with talc (and possibly additives usual) and by collecting granules at the exit of the installation.
- a variant of granulation process consists in introducing a masterbatch as described above and the remaining fraction of polyethylene in the extruder.
- compositions which are in the state of extruded granules Preference is given to compositions which are in the state of extruded granules.
- the composition according to the invention generally has a standard density (measured as defined above) greater than 940 kg / m 3 and, most often, at least equal to 945 kg / m 3 and more particularly still to 947 kg / m 3 .
- the standard density of the composition does not exceed 970 kg / m 3 and more particularly 965 kg / m 3 .
- the composition according to the invention usually has an index of fluidity, measured at 190 ° C, under a load of 5 kg according to ISO 1133 (1991) of at least 0.07 g / 10 min, the values of at least 0.1 g / 10 min being the more common.
- the flow index generally does not exceed 5 g / 10 min and the more often not 2 g / 10 min.
- composition according to the invention carried out by use in the state fused to shaped objects which have a very distinct creep resistance improved, compared with identical compositions not containing talc.
- composition according to the invention can be used according to all conventional processes for manufacturing polyethylene shaped objects, such as extrusion, extrusion blow molding, extrusion thermoforming and injection. It is well suited for injecting pipe fittings. She particularly suitable for the extrusion of tubes, in particular tubes for the transport of pressurized fluids, such as water and gas.
- the present invention therefore also relates to a method of manufacture of shaped objects from the composition according to the invention.
- the invention relates in particular to a method of manufacturing fittings for tubes by injection of a composition according to the invention. Injection of the composition according to the invention is carried out in the installations and in the usual injection conditions for compositions based on ethylene polymers at temperatures, preferably around 240 to 280 ° C.
- the invention also relates to a method for the extrusion of tubes, in particular tubes intended for the transport of fluids, in particular fluids under pressure.
- the extrusion of the composition according to the invention being from preferably in the form of extruded granules, is carried out in the installations and in the usual extrusion conditions for polymer-based compositions ethylene well known to those skilled in the art at temperatures located at around 185 to 210 ° C.
- the invention also relates to objects shaped from the composition according to the invention and, in particular the fittings for tubes obtained by injection of the composition and the tubes obtained by extrusion of the composition.
- the invention relates more particularly to tubes intended for transport of fluids, in particular pressurized fluids, shaped by extrusion of the composition according to the invention.
- the tubes manufactured using the composition according to the invention have a very good resistance to slow cracking (stress-cracking).
- This composition was granulated at a temperature of 210 ° C. on a ZSK 40 extruder-granulator (sold by the company Werner & Pfleiderer).
- the granules obtained had an MI 5 of 0.44 g / 10 min and an MVS of 951.9 kg / m 3 .
- tubes were made by extruding these granules onto a single screw extruder (Battenfeld type) at 190 ° C.
- Example 2 A composition identical to that of Example 1 was prepared except that it did not contain talc. This composition was granulated and tubes were manufactured under the same conditions as in Example 1. The granules exhibited an MI 5 of 0.43 g / 10 min and an MVS of 951.4 kg / m 3 .
- Example 1 comprising a small amount of talc makes it possible to obtain tubes having resistance to hydrostatic pressure (creep resistance) significantly improved compared to an identical composition not comprising talc.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Claims (11)
- Zusammensetzung auf der Basis von Polyethylen, ausgewählt unter den Homopolymeren des Ethylens und seinen Copolymeren, deren Gesamtmenge an Comonomer(en) 10 Mol-% nicht übersteigt, dadurch gekennzeichnet, dass das Polyethylen eine bei 23°C gemäß der Norm ASTM D 972 gemessene Standarddichte von höher als 940 kg/m3 aufweist, und dadurch, dass es Talk in einer Menge von weniger als 1 Gew.-Teil auf 100 Gew.-Teile Polyethylen umfasst.
- Zusammensetzung auf der Basis von Polyethylen gemäß Anspruch 1, dadurch gekennzeichnet, dass der Talk eine im Wesentlichen plättchenförmige Struktur aufweist.
- Zusammensetzung auf der Basis von Polyethylen gemäß den Ansprüchen 1 oder 2, dadurch gekennzeichnet, dass der Talk eine Korngrößenverteilung zwischen 0,2 und 15 Mikrometern und eine mittlere Korngröße zwischen 1 und 5 Mikrometern aufweist.
- Zusammensetzung auf der Basis von Polyethylen gemäß einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, dass die Menge an Talk zwischen 0,05 und 0,25 Gew.-Teilen auf 100 Gew.-Teile Polyethylen liegt.
- Zusammensetzung auf der Basis von Polyethylen gemäß einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, dass das Polyethylen ausgewählt ist unter den Homopolymeren und den Copolymeren des Ethylens mit insgesamt 0,01 bis 10 Mol-% Comonomeren, aufweisend eine Standarddichte, die höher als 943 kg/m3 ist und 960 kg/m3 nicht übersteigt, und einen Schmelzindex, gemessen bei 190°C unter einer Last von 5 kg gemäß der Norm ISO 1133 (1991), von 0,07 bis 5 g/10 min.
- Zusammensetzung auf der Basis von Polyethylen gemäß Anspruch 5, dadurch gekennzeichnet, dass das Polyethylen ausgewählt ist unter den Ethylencopolymeren mit insgesamt 0,05 bis 5 Mol-% Buten und/oder Hexen.
- Zusammensetzung auf der Basis von Polyethylen gemäß einem der Ansprüche 1 bis 6, dadurch gekennzeichnet, dass sie sich im Zustand von extrudiertem Granulat befindet.
- Verfahren zur Herstellung von Formteilen aus der Zusammensetzung gemäß einem der Ansprüche 1 bis 7.
- Verfahren zur Herstellung von Formteilen gemäß Anspruch 8, dadurch gekennzeichnet, dass es angewandt wird für die Extrusion von Rohren, insbesondere Rohren, die bestimmt sind für den Transport von Flüssigkeiten unter Druck, oder für das Spritzen von Verbindungsstücken für Rohre.
- Rohre, geformt durch Extrusion einer Zusammensetzung gemäß einem der Ansprüche 1 bis 7.
- Verbindungsstücke für Rohre, geformt durch Spritzen einer Zusammensetzung gemäß einem der Ansprüche 1 bis 7.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SI9830402T SI0892009T1 (sl) | 1997-07-14 | 1998-07-04 | Sestavek na osnovi polietilena in postopek za proizvodnjo izdelkov iz sestavka |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE9700619 | 1997-07-14 | ||
BE9700619A BE1011282A3 (fr) | 1997-07-14 | 1997-07-14 | Composition a base de polyethylene et procede de fabrication d'objets faconnes a partir de la composition. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0892009A1 EP0892009A1 (de) | 1999-01-20 |
EP0892009B1 true EP0892009B1 (de) | 2002-12-04 |
Family
ID=3890644
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP98202267A Expired - Lifetime EP0892009B1 (de) | 1997-07-14 | 1998-07-04 | Auf Polyethylene basierende Zusammensetzung sowie Verfahren zur Herstellung von Gegenständen aus dieser Zusammensetzung |
Country Status (26)
Country | Link |
---|---|
US (1) | US7052754B2 (de) |
EP (1) | EP0892009B1 (de) |
JP (1) | JP4084887B2 (de) |
KR (1) | KR100616354B1 (de) |
CN (1) | CN1096930C (de) |
AR (1) | AR016333A1 (de) |
AT (1) | ATE229054T1 (de) |
AU (1) | AU733340B2 (de) |
BE (1) | BE1011282A3 (de) |
BR (1) | BR9802475A (de) |
CZ (1) | CZ213098A3 (de) |
DE (1) | DE69809844T2 (de) |
DK (1) | DK0892009T3 (de) |
ES (1) | ES2186091T3 (de) |
HR (1) | HRP980392B1 (de) |
HU (1) | HUP9801553A3 (de) |
MA (1) | MA24606A1 (de) |
NO (1) | NO320566B1 (de) |
PL (1) | PL195270B1 (de) |
PT (1) | PT892009E (de) |
RU (1) | RU2219201C2 (de) |
SI (1) | SI0892009T1 (de) |
SK (1) | SK95398A3 (de) |
TN (1) | TNSN98133A1 (de) |
UA (1) | UA59355C2 (de) |
YU (1) | YU49184B (de) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2005235271A1 (en) * | 2004-04-26 | 2005-11-03 | Innate Pharma | Adjuvant composition and methods for its use |
EP1740651A1 (de) * | 2004-04-26 | 2007-01-10 | Borealis Technology Oy | Verwendung |
CA2505894A1 (en) * | 2005-04-29 | 2006-10-29 | Nova Chemicals Corporation | Method for reducing dusting in hdpe |
US7786203B2 (en) * | 2005-09-16 | 2010-08-31 | Milliken & Company | Polymer compositions comprising nucleating or clarifying agents and articles made using such compositions |
CA2741962C (en) * | 2008-10-31 | 2017-08-01 | Borealis Ag | Cross-linked polyethylene pipe |
EP2199650A1 (de) * | 2008-12-19 | 2010-06-23 | Borealis AG | Schimmelhemmendes Verfahren und Zusammensetzung |
CN103627063A (zh) * | 2012-08-29 | 2014-03-12 | 中国石油化工股份有限公司 | 一种乙烯聚合物组合物和乙烯聚合物材料以及瓶盖 |
JP6238793B2 (ja) * | 2014-03-03 | 2017-11-29 | 株式会社クレハ | フッ化ビニリデン系樹脂の溶融成形方法 |
EA202091585A1 (ru) * | 2017-12-27 | 2020-09-17 | Публичное акционерное общество "СИБУР Холдинг" | Полиэтиленовая композиция c повышенными прочностными характеристиками, способ получения указанной композиции, а также ее применение |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB822498A (en) * | 1956-06-01 | 1959-10-28 | Ici Ltd | Polyethylene films |
FR2501217B1 (fr) * | 1981-03-05 | 1985-12-27 | Charbonnages Ste Chimique | Compositions antibloquantes a base de polyethylene et films obtenus |
US4517316A (en) * | 1984-01-24 | 1985-05-14 | Dasurat Enterprises Pte Ltd. | Porous irrigation pipe prepared from particulate elastomer and thermoplastic binder containing controlled moisture content |
US4762860A (en) * | 1984-11-16 | 1988-08-09 | The Dow Chemical Company | Alcohol control of lightly crosslinked foamed polymer production |
JPS62174237A (ja) * | 1985-10-19 | 1987-07-31 | Asahi Chem Ind Co Ltd | ポリオレフイン‐ポリスチレン混合樹脂発泡体 |
JPS63260416A (ja) * | 1986-04-15 | 1988-10-27 | Japan Styrene Paper Co Ltd | 発泡成形体の製造方法 |
DE3704207A1 (de) * | 1987-02-11 | 1988-08-25 | Hoechst Ag | Polypropylen-formmasse |
US5049441A (en) * | 1989-02-21 | 1991-09-17 | Paxon Polymer Company, Lp | High density polyethylene compositions |
US5631069A (en) * | 1994-05-09 | 1997-05-20 | The Dow Chemical Company | Medium modulus molded material comprising substantially linear polyethlene and fabrication method |
US5803131A (en) * | 1994-09-26 | 1998-09-08 | Toyoda Gosei Co., Ltd. | Fuel filler pipe |
BE1008934A3 (fr) * | 1994-12-06 | 1996-10-01 | Solvay | Tube, plaque ou article bioriente. |
JPH09176328A (ja) * | 1995-12-21 | 1997-07-08 | Tonen Corp | ポリプロピレン系樹脂組成物の製造方法 |
-
1997
- 1997-07-14 BE BE9700619A patent/BE1011282A3/fr active
-
1998
- 1998-07-03 CZ CZ982130A patent/CZ213098A3/cs unknown
- 1998-07-04 DK DK98202267T patent/DK0892009T3/da active
- 1998-07-04 DE DE69809844T patent/DE69809844T2/de not_active Expired - Lifetime
- 1998-07-04 PT PT98202267T patent/PT892009E/pt unknown
- 1998-07-04 EP EP98202267A patent/EP0892009B1/de not_active Expired - Lifetime
- 1998-07-04 AT AT98202267T patent/ATE229054T1/de active
- 1998-07-04 ES ES98202267T patent/ES2186091T3/es not_active Expired - Lifetime
- 1998-07-04 SI SI9830402T patent/SI0892009T1/sl unknown
- 1998-07-07 UA UA98073601A patent/UA59355C2/uk unknown
- 1998-07-07 AU AU75025/98A patent/AU733340B2/en not_active Ceased
- 1998-07-08 KR KR1019980027398A patent/KR100616354B1/ko not_active IP Right Cessation
- 1998-07-10 SK SK953-98A patent/SK95398A3/sk unknown
- 1998-07-13 YU YU29298A patent/YU49184B/sh unknown
- 1998-07-13 NO NO19983227A patent/NO320566B1/no unknown
- 1998-07-13 PL PL327436A patent/PL195270B1/pl unknown
- 1998-07-13 AR ARP980103401A patent/AR016333A1/es not_active Application Discontinuation
- 1998-07-13 TN TNTNSN98133A patent/TNSN98133A1/fr unknown
- 1998-07-13 RU RU98113298/04A patent/RU2219201C2/ru not_active IP Right Cessation
- 1998-07-13 HU HU9801553A patent/HUP9801553A3/hu unknown
- 1998-07-14 US US09/115,229 patent/US7052754B2/en not_active Expired - Lifetime
- 1998-07-14 JP JP19842098A patent/JP4084887B2/ja not_active Expired - Fee Related
- 1998-07-14 MA MA25168A patent/MA24606A1/fr unknown
- 1998-07-14 HR HR980392A patent/HRP980392B1/xx not_active IP Right Cessation
- 1998-07-14 CN CN98116044A patent/CN1096930C/zh not_active Expired - Fee Related
- 1998-07-30 BR BR9802475A patent/BR9802475A/pt not_active Application Discontinuation
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0052555B2 (de) | Polyäthylen-Zusammensetzungen zum Extrudieren, insbesondere für das Blasverfahren | |
EP0052557B1 (de) | Polypropylen-Zusammensetzungen mit verbesserter Schlagzähigkeit | |
BE1011333A3 (fr) | Procede de fabrication d'une composition de polymeres d'ethylene. | |
BE1012775A3 (fr) | Compositions souples a base de polymeres du propylene. | |
EP1266933A1 (de) | Zusammensetzung aus Polyethylen | |
EP0892009B1 (de) | Auf Polyethylene basierende Zusammensetzung sowie Verfahren zur Herstellung von Gegenständen aus dieser Zusammensetzung | |
EP0687706A1 (de) | Polyolefin-Zusammensetzung und Verfahren zur Herstellung von Formteilen mit diesen | |
US5298537A (en) | Polyoxymethylene compositions containing at least one encapsulated nucleant | |
EP3202846A1 (de) | Polyacetalharzzusammensetzung und gleitelement | |
BE1004603A3 (fr) | Compositions moulables a base de polyolefines et objets faconnes a partir de ces compositions. | |
BE1010088A3 (fr) | Terpolymere d'ethylene, procede pour son obtention, composition consistant essentiellement en terpolymere et objets manufactures a partir de cette composition. | |
KR101374998B1 (ko) | 멀티모달 폴리에틸렌 조성물로 제조된 파이프용 층 | |
KR100792111B1 (ko) | 내크리프 특성을 갖는 파이프용 폴리에틸렌 수지조성물 | |
EP1000120A1 (de) | Zusammensetzung, die ein metallocene-plastomer mit dichte niedriger als 0.900 und ethylen-alkyl(meth)acrylat-copolymer enthält |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IT LI NL PT SE |
|
AX | Request for extension of the european patent |
Free format text: AL;LT;LV;MK;RO;SI |
|
17P | Request for examination filed |
Effective date: 19990720 |
|
AKX | Designation fees paid |
Free format text: AT BE CH DE DK ES FI FR GB GR IT LI NL PT SE |
|
AXX | Extension fees paid |
Free format text: RO PAYMENT 19990720;SI PAYMENT 19990720 |
|
17Q | First examination report despatched |
Effective date: 20010906 |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IT LI NL PT SE |
|
AX | Request for extension of the european patent |
Free format text: RO PAYMENT 19990720;SI PAYMENT 19990720 |
|
REF | Corresponds to: |
Ref document number: 229054 Country of ref document: AT Date of ref document: 20021215 Kind code of ref document: T |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 20021204 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: NV Representative=s name: KIRKER & CIE SA |
|
REF | Corresponds to: |
Ref document number: 69809844 Country of ref document: DE Date of ref document: 20030116 |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: T3 |
|
REG | Reference to a national code |
Ref country code: SE Ref legal event code: TRGR |
|
REG | Reference to a national code |
Ref country code: GR Ref legal event code: EP Ref document number: 20030400704 Country of ref document: GR |
|
REG | Reference to a national code |
Ref country code: PT Ref legal event code: SC4A Free format text: AVAILABILITY OF NATIONAL TRANSLATION Effective date: 20030225 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2186091 Country of ref document: ES Kind code of ref document: T3 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GR Payment date: 20030718 Year of fee payment: 6 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20030905 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20050203 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E |
|
BECA | Be: change of holder's address |
Owner name: *INNOVENNE MANUFACTURING BELGIUMSCHELDELAAN 482, B Effective date: 20051006 |
|
BECH | Be: change of holder |
Owner name: *INNOVENNE MANUFACTURING BELGIUM Effective date: 20051006 |
|
BECN | Be: change of holder's name |
Owner name: *INNOVENNE MANUFACTURING BELGIUMSCHELDELAAN 482, B Effective date: 20051006 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PUE Owner name: O & D BELGIUM NV Free format text: BP HIGH DENSITY POLYETHYLENE BELGIUM NV#RANSBEECKSTRAAT 310#1120 BRUSSELS (BE) -TRANSFER TO- O & D BELGIUM NV#SCHELDELAAN 482#2040 ANTWERP (BE) Ref country code: CH Ref legal event code: PFA Owner name: BP HIGH DENSITY POLYETHYLENE BELGIUM NV Free format text: SOLVAY POLYOLEFINS EUROPE - BELGIUM (SOCIETE ANONYME)#RUE DU PRINCE ALBERT, 44#1050 BRUXELLES (BE) -TRANSFER TO- BP HIGH DENSITY POLYETHYLENE BELGIUM NV#RANSBEECKSTRAAT 310#1120 BRUSSELS (BE) Ref country code: CH Ref legal event code: PFA Owner name: INNOVENE MANUFACTURING BELGIUM NV Free format text: O & D BELGIUM NV#SCHELDELAAN 482#2040 ANTWERP (BE) -TRANSFER TO- INNOVENE MANUFACTURING BELGIUM NV#SCHELDELAAN 482#2040 ANTWERPEN (BE) |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: CD |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: TP Ref country code: FR Ref legal event code: CD |
|
NLS | Nl: assignments of ep-patents |
Owner name: O & D BELGIUM NV Effective date: 20051019 |
|
NLT1 | Nl: modifications of names registered in virtue of documents presented to the patent office pursuant to art. 16 a, paragraph 1 |
Owner name: INNOVENE MANUFACTURING BELGIUM NV Owner name: BP HIGH DENSITY POLYETHYLENE BELGIUM NV |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: PT Payment date: 20060622 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20060731 Year of fee payment: 9 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PFA Owner name: INEOS MANUFACTURING BELGIUM NV Free format text: INNOVENE MANUFACTURING BELGIUM NV#SCHELDELAAN 482#2040 ANTWERPEN (BE) -TRANSFER TO- INEOS MANUFACTURING BELGIUM NV#SCHELDELAAN 482#2040 ANTWERPEN (BE) |
|
NLT1 | Nl: modifications of names registered in virtue of documents presented to the patent office pursuant to art. 16 a, paragraph 1 |
Owner name: INEOS MANUFACTURING BELGIUM NV |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: CD |
|
BECA | Be: change of holder's address |
Owner name: *INEOS MANUFACTURING BELGIUM N.V.SCHELDELAAN 482, Effective date: 20051006 |
|
BECH | Be: change of holder |
Owner name: *INEOS MANUFACTURING BELGIUM N.V. Effective date: 20051006 |
|
BECN | Be: change of holder's name |
Owner name: *INEOS MANUFACTURING BELGIUM N.V.SCHELDELAAN 482, Effective date: 20051006 |
|
REG | Reference to a national code |
Ref country code: PT Ref legal event code: MM4A Free format text: LAPSE DUE TO NON-PAYMENT OF FEES Effective date: 20080104 |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: EBP |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DK Payment date: 20060730 Year of fee payment: 9 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20080104 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070731 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070704 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E Free format text: REGISTERED BETWEEN 20120510 AND 20120516 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E Free format text: REGISTERED BETWEEN 20120628 AND 20120704 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20150726 Year of fee payment: 18 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20150727 Year of fee payment: 18 Ref country code: CH Payment date: 20150914 Year of fee payment: 18 Ref country code: FI Payment date: 20150729 Year of fee payment: 18 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20150619 Year of fee payment: 18 Ref country code: SE Payment date: 20150729 Year of fee payment: 18 Ref country code: BE Payment date: 20150727 Year of fee payment: 18 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 19 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160731 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MM Effective date: 20160801 |
|
REG | Reference to a national code |
Ref country code: SE Ref legal event code: EUG |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MM01 Ref document number: 229054 Country of ref document: AT Kind code of ref document: T Effective date: 20160704 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160801 Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160705 Ref country code: FI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160704 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160731 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160731 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160704 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E Free format text: REGISTERED BETWEEN 20170615 AND 20170621 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E Free format text: REGISTERED BETWEEN 20170622 AND 20170628 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 20 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20170727 Year of fee payment: 20 Ref country code: DE Payment date: 20170727 Year of fee payment: 20 Ref country code: FR Payment date: 20170726 Year of fee payment: 20 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20180507 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160705 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R071 Ref document number: 69809844 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: PE20 Expiry date: 20180703 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION Effective date: 20180703 |